Patent GB-842377-A (GB)
Title: Improvements in or relating to the catalytic hydrofining and/or hydrogenation of hydrocarbons
Inventor: LIMIDO JEAN
IPC: C07C5/10
Filed: 1958-02-17
Abstract: Unsaturated or aromatic hydrocarbons or fractions containing them having a mean molecular weight of 25-200 are catalytically hydrogenated or hydrofined by treating in the liquid phase in solution in an inert hydrocarbon having a boiling point above 220 DEG C. and sufficiently above the boiling points of the starting materials and final products to permit easy fractionation of the latter with hydrogen in the presence of a hydrogenation catalyst. The solvent may be for example paraffins, napthenes such as alkyldecahydronaphthalenes, alkylcyclohexanes or dicyclohexyl, aromatic hydrocarbons such as alkyl benzenes, alkyl naphthalenes, dibenzyl, diphenyl and alkyl diphenyls, and hydrocarbon fractions such as paraffinic concentrates from treatment with urea, phenol or furfurol and distillationfractions of coal tars and washing oils or petroleum distillates such as gas oil and lubricating oils. Hydrofining is preferably carried out at 250-500 DEG C. and 10-250 atmospheres with a hydrogen partial pressure in the gaseous phase above the solution of more than 3 atmospheres in the presence of catalysts such as the oxides and sulphides of Group VI and VIII metals.  Hydrogenation of unsaturated or aromatic compounds to saturated compounds may be performed at 100-250 DEG C. and up to 50 atmospheres using a Group VIII metallic catalyst and the compound is preferably first purified by a hydrofining technique according to the invention.  Contact of the gaseous and liquid phases may be achieved by mechanised agitation or by the kinetic energy of the incoming reactants.  In one embodiment the catalyst is suspended in the solvent in a tubular reactor and the unsaturated hydrocarbon and hydrogen are introduced at the bottom; products are then recovered as vapours at the top of the reactor.ALSO:Unsaturated or aromatic hydrocarbons or fractions containing them having a mean molecular weight of 25-200 are catalytically hydrogenated or hydrofined by treating in the liquid phase in solution in an inert hydrocarbon having a boiling point above 220 DEG C. and sufficiently above the boiling points of the starting materials and final products to permit easy fractionation of the latter with hydrogen in the presence of a hydrogenation catalyst. The solvent may be for example paraffins, naphthenes such as alkyldecahydronaphthalenes, alkylcyclohexanes or dicyclohexyl, aromatic hydrocarbons such as alkyl benzenes, alkyl naphthalenes, dibenzyl, diphenyl and alkyl diphenyls, and hydrocarbon fractions such as paraffinic concentrates from treatment with urea, phenol or furfurol and distillation fractions of coal tars and washing oils or petroleum distillates such as gas oil and lubricating oils.  Hydrofining is preferably carried out at 250-500 DEG C. and 10-250 atmospheres with a hydrogen partial pressure in the gaseous phase above the solution of more than 3 atmospheres in the presence of catalysts such as the oxides and sulphides of Group VI and VIII metals e.g. Co, Mo, Cr or W, which may be supported e.g. on active carbon or alumina.  Hydrogenation of unsaturated or aromatic compounds to saturated compounds may be performed at 100-250 DEG C. and up to 50 atmospheres using a Group VIII metallic catalyst and the compound is preferably first purified by a hydrofining technique according to the invention.  Contact of the gaseous and liquid phases may be achieved by mechanised agitation or by the kinetic energy of the incoming reactants.  In one embodiment the catalyst is suspended in the solvent in a tubular reactor and the unsaturated hydrocarbon and hydrogen are introduced at the bottom; products are then recovered as vapours at the top of the reactor.